EP2820170B1 - A zeolite coating preparation assembly and operation method - Google Patents
A zeolite coating preparation assembly and operation method Download PDFInfo
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- EP2820170B1 EP2820170B1 EP13717561.8A EP13717561A EP2820170B1 EP 2820170 B1 EP2820170 B1 EP 2820170B1 EP 13717561 A EP13717561 A EP 13717561A EP 2820170 B1 EP2820170 B1 EP 2820170B1
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- 238000000576 coating method Methods 0.000 title claims description 74
- 239000011248 coating agent Substances 0.000 title claims description 52
- 239000010457 zeolite Substances 0.000 title claims description 52
- 229910021536 Zeolite Inorganic materials 0.000 title claims description 49
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 title claims description 49
- 238000000034 method Methods 0.000 title claims description 34
- 238000002360 preparation method Methods 0.000 title claims description 17
- 239000000758 substrate Substances 0.000 claims description 54
- 230000015572 biosynthetic process Effects 0.000 claims description 49
- 238000003786 synthesis reaction Methods 0.000 claims description 45
- 230000006698 induction Effects 0.000 claims description 30
- 238000010438 heat treatment Methods 0.000 claims description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 18
- 238000006243 chemical reaction Methods 0.000 claims description 10
- 230000005291 magnetic effect Effects 0.000 claims description 10
- 239000000463 material Substances 0.000 claims description 10
- 238000004140 cleaning Methods 0.000 claims description 4
- 230000000694 effects Effects 0.000 claims description 4
- 239000003302 ferromagnetic material Substances 0.000 claims description 3
- 239000000376 reactant Substances 0.000 claims description 3
- 238000011049 filling Methods 0.000 claims description 2
- 239000012467 final product Substances 0.000 claims description 2
- 239000004020 conductor Substances 0.000 claims 1
- 239000002184 metal Substances 0.000 description 7
- 229910052751 metal Inorganic materials 0.000 description 7
- 239000000203 mixture Substances 0.000 description 6
- 238000009792 diffusion process Methods 0.000 description 5
- 239000011541 reaction mixture Substances 0.000 description 5
- 238000006555 catalytic reaction Methods 0.000 description 4
- 238000001179 sorption measurement Methods 0.000 description 4
- 239000013078 crystal Substances 0.000 description 3
- 238000002425 crystallisation Methods 0.000 description 3
- 230000008025 crystallization Effects 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 229910001220 stainless steel Inorganic materials 0.000 description 3
- 239000010935 stainless steel Substances 0.000 description 3
- 230000009466 transformation Effects 0.000 description 3
- 239000003463 adsorbent Substances 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 239000013335 mesoporous material Substances 0.000 description 2
- 239000012229 microporous material Substances 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000003889 chemical engineering Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 239000000499 gel Substances 0.000 description 1
- 238000005216 hydrothermal crystallization Methods 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
- 229920005992 thermoplastic resin Polymers 0.000 description 1
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
- B01J20/3231—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
- B01J20/3234—Inorganic material layers
- B01J20/3238—Inorganic material layers containing any type of zeolite
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/08—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
- B01J19/087—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electric or magnetic energy
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C18/00—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
- C23C18/02—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by thermal decomposition
- C23C18/12—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by thermal decomposition characterised by the deposition of inorganic material other than metallic material
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C18/00—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
- C23C18/02—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by thermal decomposition
- C23C18/12—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by thermal decomposition characterised by the deposition of inorganic material other than metallic material
- C23C18/1204—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by thermal decomposition characterised by the deposition of inorganic material other than metallic material inorganic material, e.g. non-oxide and non-metallic such as sulfides, nitrides based compounds
- C23C18/1208—Oxides, e.g. ceramics
- C23C18/1212—Zeolites, glasses
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C18/00—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
- C23C18/02—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by thermal decomposition
- C23C18/12—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by thermal decomposition characterised by the deposition of inorganic material other than metallic material
- C23C18/125—Process of deposition of the inorganic material
- C23C18/1287—Process of deposition of the inorganic material with flow inducing means, e.g. ultrasonic
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C18/00—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
- C23C18/02—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by thermal decomposition
- C23C18/12—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by thermal decomposition characterised by the deposition of inorganic material other than metallic material
- C23C18/125—Process of deposition of the inorganic material
- C23C18/1291—Process of deposition of the inorganic material by heating of the substrate
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C18/00—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
- C23C18/14—Decomposition by irradiation, e.g. photolysis, particle radiation or by mixed irradiation sources
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/08—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
- B01J2219/0803—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electric or magnetic energy
- B01J2219/085—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electric or magnetic energy creating magnetic fields
Definitions
- the present invention relates to a zeolite coating preparation assembly and operation method wherein zeolite adsorbents are coated by crystallization process on various surfaces heated by induction.
- Zeolites are synthesized from a reaction mixture by means of hydrothermal crystallization.
- a reaction mixture is prepared by mixing suitable proportions of the required reactants in order to obtain the aimed zeolite type.
- this mixture is heated, at the end of certain periods of time, nuclei of the zeolite crystals are formed and then the crystals start to grow.
- the nuclei/crystals often chemically bind with this substrate and form a zeolite coating which is strongly attached thereon. Properties of this coating depend on the composition of the reaction mixture that is used, and the experimental conditions such as reaction temperature and time and mixing.
- Use of dilute solutions as the reaction mixture instead of highly viscous gels used in conventional zeolite synthesis has a positive impact on the coating quality.
- zeolites are metastable materials
- a zeolite phase synthesized from a reaction composition transforms into other phases after longer reaction times. This situation impedes the coatings from being sufficiently thick when the conventional single step synthesis method is used for many zeolite phases.
- composition of the solution changes as the time increases, as a result of the crystallization activity in the reaction solution, preparing a thick coating is still not easy.
- Multi-step methods that may be used for preparation of thick coatings are not practical or economical. Additionally, strength of the thick coatings is also low when these methods are used and the coatings have a very compact structure that will make diffusion difficult.
- the reaction solution is kept at a temperature that is lower than the reaction temperature by the help of a water bath.
- phase transformation of the zeolite is delayed for long periods of time and thus thicker coatings can be obtained in comparison to the conventional methods.
- These coatings also have an open structure, high diffusion coefficient and relatively higher stability which are necessary for many applications, especially for adsorption heat pump applications.
- Chinese Patent document no. CN101754508 an application known in the art, discloses an induction heater used for coating steel surfaces.
- the system includes independent induction heaters and on the upper parts thereof copper coils. Water nozzles are provided at the head ends and the tail ends of the induction coils.
- the said heater has a simple structure and a high efficiency.
- Japanese patent document no. JP2006256066 an application in the state of the art, discloses a method for coating the surface of a substrate with a resin. During coating, the resin acquires the shape of the surface and this shape can be maintained. In the contact process used in the method, the material containing a thermoplastic resin is ensured to contact the surface of the conductive substrate. Then temperature of the substrate surface is increased by means of the induction heater.
- XU X ET AL "Synthesis of a high-permeance NaA zeolite membrane by microwave heating", ADVANCED MATERIALS, vol. 12, no. 3, 195-198 (2000 ) discloses the formation of a zeolite coating on a substrate through application of a microwave radiation.
- the objective of the present invention relates to a zeolite coating preparation assembly and operation method by which synthesis process is shortened owing to heating by induction and this way time is saved.
- Another objective of the present invention relates to a zeolite coating preparation assembly and operation method, by which material saving is achieved since large heating resistances and complicated reactors are not used, and which is thus more economical.
- a further objective of the present invention relates to a zeolite coating preparation assembly and operation method for preparing a zeolite coating with desired thickness in shorter periods of time relative to the known methods.
- Another objective of the present invention relates to a zeolite coating preparation assembly and operation method wherein the coatings are obtained in a thicker and more stable form by using a more practical and suitable reaction system.
- Another objective of the present invention relates to a zeolite coating preparation assembly and operation method wherein mass production is enabled.
- the inventive zeolite coating assembly (1) according to claim 1 comprises:
- temperature of the synthesis solution (3) is changed by means of a water bath (S) in which the feeding tank (7) is immersed, in such a way that the heat exchanger (8) does not directly contact the synthesis solution (3) so that chemical composition of the synthesis solution (3) is not affected.
- a reactor (2) made of a material with a low electrical conductivity is used for preventing zeolite formation on the reactor (2) walls and preventing the heated reactor (2) from unnecessarily heating the synthesis solution (3).
- the synthesis solution (3) is prepared as diluted in order to enhance the quality of the coating.
- the water bath (S) temperature is adjusted so as to keep the temperature of the synthesis solution (3) in the reactor (2) at a desired value that is lower than the temperature of the substrate (4).
- a substrate (4) which has a high electrical conductivity and is preferably made of a ferromagnetic material, is used in order to enhance the effect of the magnetic field generated by the induction device (5) on coating formation.
- the substrate (4) is vertically immersed within the synthesis solution (3) in the reactor (2) in order to increase the coating thickness, coating stability and the effective diffusion coefficient of the coating.
- the inventive zeolite coating method according to claim 4 comprises the steps of
- the reactor (2) dimensions are determined according to the substrate (4) size and solution (3) amount to be used, and the reactor (2) prepared for synthesis reaction is made ready for use.
- a synthesis solution (3) suitable for the zeolite type that is desired to be obtained is prepared.
- the substrate (4) is made ready for use by being cleaned with suitable methods, it is vertically immersed in the synthesis solution (3) that is filled into the reactor (2).
- the reactor (2) is positioned such that the substrate (4) therein will remain within the magnetic field generated by the coil (6) connected to the induction device (5). Taking into account the possible reactor (2) dimensions, it is considered that it will be more suitable to keep the reactor (2) out of the coil (6).
- the distance between the coil (6) and the reactor (2) or the power of the induction device (5) is changed and adjusted so as to obtain the desired substr distance (mm)
- This temperature together with the solution (3) temperature and synthesis time, determines the zeolite phase and the coating thickness which will be obtained.
- the substrate (4) temperature is approximately 65°C
- the substrate (4) temperature is 55°C
- the substrate (4) temperature is 45°C ( Figure 2 ).
- the synthesis solution (3) is circulated by the help of a pump (9) between the water bath (S) having a temperature lower than the reaction temperature and the reactor (2). This way, the solution (3) is enabled to be kept at a temperature lower than that of the substrate (4) and the reaction is enabled to be concentrated not in the solution (3) but on the substrate (4). Although the synthesis solution (3) is not actually affected by the magnetic field, the heated substrate (4) also heats the solution (3) to some degree.
- the solution (3) temperature is approximately 35°C
- the solution (3) temperature is 30°C
- the solution (4) temperature is 25°C ( Figure 3 ).
- a magnetic field is produced around the substrate (4) by operating the induction device (5). Under the said conditions, the synthesis reaction within the reactor (2), whose top is covered, is carried out for a period of time that will allow generation of the desired phase.
- the substrate (4) which is coated with zeolite is removed from the system, washed with water and made ready for use.
- the assembly (1) of the present invention By means of the assembly (1) of the present invention, mass production can be carried out more economically and practically.
- the system of heating by induction performed in the assembly (1) of the present invention is practical; because, differing from the state of the art applications, it does not require large heating resistances and complicated reactors for coating large surfaces.
- the fact that the inventive method is economical is based on the fact that the period of time for obtaining a zeolite coating with the same coating thickness and at the same synthesis temperature via heating by induction is much shorter in comparison to the conventional methods and method of heating by conduction. For example, while zeolite A coating reaches a thickness of 100 ⁇ m at the end of 72 hours when heating is performed by conduction, the coating thickness reaches 210 ⁇ m within 6 hours when heating is performed by induction under the same conditions.
- This method can be employed for preparing thick zeolite coatings that may be used in applications related to adsorption and catalysis. It is especially very suitable for production of zeolite coatings with the necessary characteristics for adsorption heat pumps. Additionally, this method can also be used for preparation of thin or thick coatings of the other adsorbents which can be directly obtained from a solution via crystallization.
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- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Inorganic Chemistry (AREA)
- Metallurgy (AREA)
- General Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
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- General Health & Medical Sciences (AREA)
- Health & Medical Sciences (AREA)
- Analytical Chemistry (AREA)
- Ceramic Engineering (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Application Of Or Painting With Fluid Materials (AREA)
- Other Surface Treatments For Metallic Materials (AREA)
- Coating Apparatus (AREA)
Description
- The present invention relates to a zeolite coating preparation assembly and operation method wherein zeolite adsorbents are coated by crystallization process on various surfaces heated by induction.
- Zeolites are synthesized from a reaction mixture by means of hydrothermal crystallization. A reaction mixture is prepared by mixing suitable proportions of the required reactants in order to obtain the aimed zeolite type. When this mixture is heated, at the end of certain periods of time, nuclei of the zeolite crystals are formed and then the crystals start to grow. When there is a substrate in the medium immersed in the reaction mixture, the nuclei/crystals often chemically bind with this substrate and form a zeolite coating which is strongly attached thereon. Properties of this coating depend on the composition of the reaction mixture that is used, and the experimental conditions such as reaction temperature and time and mixing. Use of dilute solutions as the reaction mixture instead of highly viscous gels used in conventional zeolite synthesis has a positive impact on the coating quality.
- Since zeolites are metastable materials, a zeolite phase synthesized from a reaction composition transforms into other phases after longer reaction times. This situation impedes the coatings from being sufficiently thick when the conventional single step synthesis method is used for many zeolite phases. In cases where metastable phase transformation does not occur, since composition of the solution changes as the time increases, as a result of the crystallization activity in the reaction solution, preparing a thick coating is still not easy. Multi-step methods that may be used for preparation of thick coatings are not practical or economical. Additionally, strength of the thick coatings is also low when these methods are used and the coatings have a very compact structure that will make diffusion difficult.
- In the method of direct heating of the substrate by conduction, wherein the substrate is heated by the help of a resistance (one of the state-of-the-art applications), the reaction solution is kept at a temperature that is lower than the reaction temperature by the help of a water bath. In this manner, phase transformation of the zeolite is delayed for long periods of time and thus thicker coatings can be obtained in comparison to the conventional methods. These coatings also have an open structure, high diffusion coefficient and relatively higher stability which are necessary for many applications, especially for adsorption heat pump applications.
- There are several articles in the literature related to direct heating of the substrate materials by using the method of heating by conduction: "Erdem-enatalar, A., Tatlier, M., Ürgen, M., "Preparation of Zeolite Coatings by Direct Heating of the Substrates", Microporous and Mesoporous Materials, 32(3), 331-343 (1999)"; "Tatlier, M., Erdem-enatalar, A., "The Stability of Zeolite Coatings Grown on Metal Supports for Heat Pump Applications", Studies in Surface Science and Catalysis, Vol. 125, Elsevier, Amsterdam, 101-108 (1999)"; "Tatlier, M., Tantekin-Ersolmaz, .B., Erdem-enatalar, A., "Diffusivities of Zeolite Coatings", (Proc. 13th International Zeolite Conference, 2001, Montpellier, France), A. Galarneau, F.Di Renzo, F. Fajula, J. Vedrine (ed.), Studies in Surface Science and Catalysis, Vol. 135, Elsevier, Amsterdam, 3249-3256 (2001)"; "Erdem-enatalar, A., Oner, K., Tatlier, M., "Searching for Clear Solution Compositions by Using the Substrate Heating Method", Studies in Surface Science and Catalysis, Vol. 154 part A-C, 667-670 (2004)"; "Tatlier, M., Erdem-enatalar, A., "Estimation of the Effective Diffusion Coefficients in Open Zeolite Coatings", Chemical Engineering Journal, 102(3), 209-216 (2004)"; "Tatlier, M., Demir, M., Tokay, B., Erdem-enatalar, A., Kiwi-Minsker, L., "Substrate Heating Method for Coating Metal Surfaces with High-Silica Zeolites: ZSM-5 Coatings on Stainless Steel Plates", Microporous and Mesoporous Materials, 101(3), 374-380 (2007)"; Schnabel, L., Tatlier, M., Schmidt, F., Erdem-enatalar, A., "Adsorption Kinetics of Zeolite Coatings Directly Crystallized on Metal Supports for Heat Pump Applications", Applied Thermal Engineering, 30(11/12), 1409-1416 (2010)".
- International patent document no.
WO2010120738 , an application known in the art, discloses a method of coating a metal surface with a protective metal coating having a lower melting point. After the surface to be coated is heated up to the melting point of the metal coating in a high frequency induction heater, the molten metal coating is immediately applied on the heated surface. - Chinese Patent document no.
CN101754508 , an application known in the art, discloses an induction heater used for coating steel surfaces. The system includes independent induction heaters and on the upper parts thereof copper coils. Water nozzles are provided at the head ends and the tail ends of the induction coils. The said heater has a simple structure and a high efficiency. - Japanese patent document no.
JP2006256066 - XU X ET AL: "Synthesis of a high-permeance NaA zeolite membrane by microwave heating", ADVANCED MATERIALS, vol. 12, no. 3, 195-198 (2000) discloses the formation of a zeolite coating on a substrate through application of a microwave radiation.
- The objective of the present invention relates to a zeolite coating preparation assembly and operation method by which synthesis process is shortened owing to heating by induction and this way time is saved.
- Another objective of the present invention relates to a zeolite coating preparation assembly and operation method, by which material saving is achieved since large heating resistances and complicated reactors are not used, and which is thus more economical.
- A further objective of the present invention relates to a zeolite coating preparation assembly and operation method for preparing a zeolite coating with desired thickness in shorter periods of time relative to the known methods.
- Another objective of the present invention relates to a zeolite coating preparation assembly and operation method wherein the coatings are obtained in a thicker and more stable form by using a more practical and suitable reaction system.
- Another objective of the present invention relates to a zeolite coating preparation assembly and operation method wherein mass production is enabled.
- "A zeolite coating preparation assembly and operation method" developed to fulfill the objective of the present invention is illustrated in the accompanying figures, in which;
-
Figure 1 is the schematic view of the zeolite coating assembly. -
Figure 2 is the representation of the change in the substrate (4) temperature according to the distance between the substrate (4) and the coil (6). -
Figure 3 is the representation of the change in the solution (4) temperature according to the distance between the substrate (3) and the coil (6). - The components shown in the figure are each given reference numbers as follows:
- 1. Zeolite coating assembly
- 2. Reactor
- 3. Synthesis solution
- 4. Substrate
- 5. Induction device
- 6. Coil.
- 7. Feeding tank
- 8. Heat exchanger
- 9. Pump
- 10. Connection line
- The inventive zeolite coating assembly (1) according to
claim 1 comprises: - at least one reactor (2) wherein the reaction is carried out and which is a container lidded on top,
- synthesis solution (3) which is filled into the reactor (2) and which includes the reactants that are used for preparing the zeolite coating,
- at least one substrate (4) which is immersed in the synthesis solution (3) and which is preferably in the form of a flat plate,
- at least one induction device (5) which is located outside of the reactor (2) and is positioned near the reactor (2) such that the magnetic field that it generates by passing electric current over its coil (6) is located at a distance that will affect the substrate (4) within the reactor (2),
- at least one feeding tank (7) in the form of a container by which a part of the synthesis solution (3) is kept outside of the reactor (2),
- at least one heat exchanger (8) which is directly or indirectly in contact with the feeding tank (7) and which changes the temperature of the synthesis solution (3) within the feeding tank (7),
- at least one pump (9) which enables circulation of the synthesis solution (3) via a connection line (10) lying between the feeding tank (7) and the reactor (2).
- In the preferred embodiment of the invention, temperature of the synthesis solution (3) is changed by means of a water bath (S) in which the feeding tank (7) is immersed, in such a way that the heat exchanger (8) does not directly contact the synthesis solution (3) so that chemical composition of the synthesis solution (3) is not affected.
- In the embodiment of the invention, a reactor (2) made of a material with a low electrical conductivity is used for preventing zeolite formation on the reactor (2) walls and preventing the heated reactor (2) from unnecessarily heating the synthesis solution (3).
- In the embodiment of the invention, the synthesis solution (3) is prepared as diluted in order to enhance the quality of the coating.
- In the preferred embodiment of the invention, in order to prevent metastable phase transformation and to enable the preparation of thick coatings, the water bath (S) temperature is adjusted so as to keep the temperature of the synthesis solution (3) in the reactor (2) at a desired value that is lower than the temperature of the substrate (4).
- In the preferred embodiment of the invention, a substrate (4), which has a high electrical conductivity and is preferably made of a ferromagnetic material, is used in order to enhance the effect of the magnetic field generated by the induction device (5) on coating formation.
- In the preferred embodiment of the invention, the substrate (4) is vertically immersed within the synthesis solution (3) in the reactor (2) in order to increase the coating thickness, coating stability and the effective diffusion coefficient of the coating.
- The inventive zeolite coating method according to
claim 4 comprises the steps of - determining and preparing the reactor (2),
- preparing the synthesis solution (3) and filling it into the reactor (2),
- cleaning the substrate (4) with suitable methods and placing it in the solution (3) filled into the reactor (2),
- placing the reactor (2) near the coil (6) of the induction device (5),
- adjusting the distance between the coil (6) and the reactor (2) and/or the power of the induction device (5) so as to provide the desired substrate (4) temperature,
- circulating the synthesis solution (3) that is in the reactor (2) by the help of a pump (9) between the water bath (S) and the reactor (2),
- adjusting the water bath (S) temperature so as to keep the temperature of the synthesis solution (3) in the reactor (2) at a desired value that is lower than the temperature of the substrate (4),
- producing magnetic field by operating the induction device (5),
- performing the synthesis at the desired temperature and time,
- removing the substrate (4) from the solution (3),
- cleaning the coating with water,
- obtaining the final product.
- The reactor (2) dimensions are determined according to the substrate (4) size and solution (3) amount to be used, and the reactor (2) prepared for synthesis reaction is made ready for use. A synthesis solution (3) suitable for the zeolite type that is desired to be obtained is prepared. After the substrate (4) is made ready for use by being cleaned with suitable methods, it is vertically immersed in the synthesis solution (3) that is filled into the reactor (2). The reactor (2) is positioned such that the substrate (4) therein will remain within the magnetic field generated by the coil (6) connected to the induction device (5). Taking into account the possible reactor (2) dimensions, it is considered that it will be more suitable to keep the reactor (2) out of the coil (6). The distance between the coil (6) and the reactor (2) or the power of the induction device (5) is changed and adjusted so as to obtain the desired substr distance (mm) This temperature, together with the solution (3) temperature and synthesis time, determines the zeolite phase and the coating thickness which will be obtained. For example, in the system that is used, for a power value of 2 kW and a stainless steel substrate, when the distance between the substrate (4) and the coil (6) is 6 mm the substrate (4) temperature is approximately 65°C, when it is 8 mm the substrate (4) temperature is 55°C and when it is 9 mm the substrate (4) temperature is 45°C (
Figure 2 ). - The synthesis solution (3) is circulated by the help of a pump (9) between the water bath (S) having a temperature lower than the reaction temperature and the reactor (2). This way, the solution (3) is enabled to be kept at a temperature lower than that of the substrate (4) and the reaction is enabled to be concentrated not in the solution (3) but on the substrate (4). Although the synthesis solution (3) is not actually affected by the magnetic field, the heated substrate (4) also heats the solution (3) to some degree. For example, when the water bath (S) temperature is 10°C, for a power value of 2 kW, when the distance between the substrate (4) and the coil (6) is 6 mm the solution (3) temperature is approximately 35°C, when it is 8 mm the solution (3) temperature is 30°C and when it is 9 mm the solution (4) temperature is 25°C (
Figure 3 ). - A magnetic field is produced around the substrate (4) by operating the induction device (5). Under the said conditions, the synthesis reaction within the reactor (2), whose top is covered, is carried out for a period of time that will allow generation of the desired phase. The substrate (4) which is coated with zeolite is removed from the system, washed with water and made ready for use.
- In the method of directly heating the substrate (4) materials by conduction, the experiment duration required for obtaining thick coatings is fairly long. Furthermore, method of heating by conduction is not practical for coating large surfaces. In the inventive zeolite coating method and assembly, when the substrate (4) materials are heated remotely by induction, thick coatings with high effective diffusion coefficients are produced.
- By means of the assembly (1) of the present invention, mass production can be carried out more economically and practically. The system of heating by induction performed in the assembly (1) of the present invention is practical; because, differing from the state of the art applications, it does not require large heating resistances and complicated reactors for coating large surfaces. The fact that the inventive method is economical is based on the fact that the period of time for obtaining a zeolite coating with the same coating thickness and at the same synthesis temperature via heating by induction is much shorter in comparison to the conventional methods and method of heating by conduction. For example, while zeolite A coating reaches a thickness of 100 µm at the end of 72 hours when heating is performed by conduction, the coating thickness reaches 210 µm within 6 hours when heating is performed by induction under the same conditions. When the conventional one-step method is used, 2-3 µm thickness is obtained at most. While zeolite X coating reaches a thickness of 110 µm within 48 hours via conventional synthesis, the said thickness is obtained within 4 hours when heating is performed by induction under the same conditions.
- As a result of the experiments conducted related to the method of the present invention, it is observed that when heating by induction is applied, crystalline and thick zeolite A (210 µm) and zeolite X (110 µm) coatings in pure form are obtained on stainless steel.
- This method can be employed for preparing thick zeolite coatings that may be used in applications related to adsorption and catalysis. It is especially very suitable for production of zeolite coatings with the necessary characteristics for adsorption heat pumps. Additionally, this method can also be used for preparation of thin or thick coatings of the other adsorbents which can be directly obtained from a solution via crystallization.
- Within the scope of these basic concepts, it is possible to develop various embodiments of the inventive "A zeolite coating preparation assembly (1) and operation method". The invention can not be limited to the examples described herein and it is essentially as defined in the claims.
Claims (6)
- A zeolite coating preparation assembly (1) characterized by- at least one reactor (2), wherein the reaction is carried out, and wherein heating by induction is performed accompanied by circulation of the synthesis solution (3), and which is a container lidded on top, and which is made of a material with a low electrical conductivity for preventing zeolite formation on the walls thereof and preventing heating of the synthesis solution (3),- synthesis solution (3) which is filled into the reactor (2), which includes the reactants that are used to prepare the zeolite coating, which is prepared as diluted in order to increase the quality of the coating, and which is circulated throughout the assembly (1),- at least one substrate (4) made of an electrically conductive material, which is immersed in the synthesis solution (3) and heated from a distance by induction to a temperature higher than that of the synthesis solution (3),- at least one induction device (5) which is located outside of the reactor (2) and is positioned near the reactor (2) at such a distance that the magnetic field that it generates by passing electric current over its coil (6) will heat the substrate (4) within the reactor (2),- at least one feeding tank (7) in the form of a container, which is placed in a water bath (S) outside of the reactor (2), and through which the synthesis solution (3) is circulated in order to keep its temperature lower than that of the substrate (4),- at least one heat exchanger (8) which is placed in the water bath (S) and which changes the temperature of the water bath (S) in order to keep the temperature of the synthesis solution (3) within the feeding tank (7) immersed in the water bath (S) at such a value that the temperature of the synthesis solution (3) in the reactor (2) remains lower than the temperature of the substrate (4),- at least one pump (9) which enables circulation of the synthesis solution (3) via a connection line (10) lying between the feeding tank (7) and the reactor (2).
- A zeolite coating preparation assembly (1) according to claim 1, characterized by a substrate (4) made of a ferromagnetic material in order to enhance the effect of the magnetic field generated by the induction device (5) on coating formation.
- A zeolite coating preparation assembly (1) according to any one of the preceding claims, characterized by a substrate (4) which is vertically immersed within the synthesis solution (3) in the reactor (2) in order to increase the coating stability.
- A zeolite coating preparation method, which is performed using the assembly (1) described in claim 1, characterized by the steps of- preparing the reactor (2), which is made of a material with low electrical conductivity,- preparing the synthesis solution as diluted (3) and filling it into the reactor (2),- cleaning the electrically conductive substrate (4) and placing it in the solution (3) filled into the reactor (2),- placing the reactor (2) near the coil (6) of the induction device (5),- adjusting the distance between the coil (6) and the reactor (2) and/or the power of the induction device (5) so as to provide the desired substrate (4) temperature,- circulating the synthesis solution (3) that is in the reactor (2) by the help of a pump (9) via the connection line (10) lying between the feeding tank (7) which is immersed in the water bath (S), and the reactor (2),- adjusting the water bath (S) temperature with the help of the heat exchanger (8) in order to keep the temperature of the synthesis solution (3) in the feeding tank (7) at a value to assure that the temperature of the synthesis solution (3) in the reactor (2) remains at a desired value that is lower than the temperature of the substrate (4),- producing magnetic field by operating the induction device (5),- performing the synthesis at the desired substrate (4) and solution (3) temperatures and time,- removing the substrate (4) from the solution (3),- cleaning the coating with water,- obtaining the final product.
- A method according to claim 4, characterized by using a substrate (4) made of a ferromagnetic material in order to enhance the effect of the magnetic field generated by the induction device (5) on coating formation.
- A method according to claims 4 and 5, characterized by using a substrate (4) which is vertically immersed within the synthesis solution (3) in the reactor (2) in order to increase the coating stability.
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PCT/IB2013/051515 WO2013128366A2 (en) | 2012-02-28 | 2013-02-25 | A zeolite coating preparation assembly and operation method |
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WO2015171727A1 (en) * | 2014-05-07 | 2015-11-12 | E. I. Du Pont De Nemours And Company | Polyimide web separator for use in an electrochemical cell |
CN105582870A (en) | 2015-11-09 | 2016-05-18 | 陕西科技大学 | Preparation method of composite material having remarkably-improved composite material interface bonding effect |
US10307726B1 (en) | 2016-11-15 | 2019-06-04 | Rodolfo Palombo | Magnetic chemical reactor |
WO2020122826A1 (en) | 2018-12-13 | 2020-06-18 | Inventram Fikri Mulkiyet Haklari Yonetim Ticaret Ve Yatirim Anonim Sirketi | A zeolite coating preparation assembly and method for operating the same |
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KR100247664B1 (en) * | 1997-09-22 | 2000-03-15 | 손욱 | Method of manufacturing silica thin film |
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US20150024924A1 (en) | 2015-01-22 |
JP6019141B2 (en) | 2016-11-02 |
CN104428446A (en) | 2015-03-18 |
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WO2013128366A3 (en) | 2014-04-17 |
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